A filtering multilayer is described, having at least two layers, one input layer and one output layer, made of non-woven fabric, wherein each fiber of said non-woven fabric consists of a polymer matrix of thermoplastic material, wherein the average diameter of the fibers that form the input layer is larger than the average diameter of the fibers that form the output layer, characterized in that the diameters of the fibers that form the input layer and the output layer have a gaussian distribution, wherein the diameter of the single fibers that form said input layer varies around the average with a normal distribution of width at least equal to 10% of the average value and the diameter of the single fibers that form said output layer varies around the average with a normal distribution of width at least equal to 14% of the average value. In a preferred embodiment, said polymer matrix contains a carbon-based filler or additive, preferably in the form of powder.
|
1. A filtering multilayer comprising one input layer and one output layer made of non-woven fabric comprising fibers, wherein each fiber of said non-woven fabric consists of a polymer matrix of thermoplastic material, wherein the average diameter of the fibers that form the input layer is larger than the average diameter of the fibers that form the output layer,
characterized in that the diameters of the fibers that form the input layer and the output layer have a gaussian distribution, wherein the diameter of each of the fibers that form said input layer varies around the average with a normal distribution of width at least equal to 10% of the average value and the diameter of each of the fibers that form said output layer varies around the average with a normal distribution of width at least equal to 14% of the average value.
2. A filtering multilayer according to
3. A filtering multilayer according to
4. A filtering multilayer according to
5. A filtering multilayer according to
6. A filtering multilayer according to
7. A filtering multilayer according to
8. A filtering multilayer according to
9. A filtering multilayer according to
10. A filtering multilayer according to
11. A filtering multilayer according to
12. A filtering multilayer according to
13. A filtering multilayer according to
14. A method for obtaining a filtering multilayer according to
a) providing a polymer fiber with which a layer of non-woven fabric is prepared, wherein the fibers in said layer have an average diameter of between 6 and 15 μm and the distribution of the diameter of the fibers that form said layer varies about the average with a normal distribution of width at least equal to 10;
b) providing a polymer fiber, wherein said fiber is of the same or a of different material with respect to the fiber in step a), with which a layer of non-woven fabric is prepared, wherein the fibers in said layer have an average diameter of between 1 and 6 μm, and the distribution of the diameter of the fibers that form said layer varies about the average with a normal distribution of width at least equal to 14% of the average value;
c) joining said layer obtained in a) with said layer obtained in b).
|
|||||||||||||||||||||||||||||||
This application claims the priority to Italian Application No. 102015000016798 filed May 22, 2015, and Italian Application No. 102015000016829 filed May 22, 2015, the entire disclosures of which are expressly incorporated herein by reference.
Filtering materials are used for removing undesired material from a fluid, forcing the flow of fluid through the filter.
In the prior art, glass microfiber is widely used in filtration. Glass microfiber ensures a high mechanical, chemical and physical resistance with good filtering performance. The drawbacks that have always accompanied the use of this material are related to the non-incinerability and to the hazard to the health and safety of the people involved in the various production steps.
Polymer microfibers assembled to form multilayer filters have been proposed as an alternative. These filters obviate the environmental problem by excluding the use of fiberglass and maintaining acceptable filtering efficiency features.
However, a problem is strongly felt when using this type of product alternative to fiberglass: an accumulation capacity lower than that observed using fiberglass.
WO2007126621 describes a multilayer filtering system wherein the fibers are made of polybutylene naphthalate (PBN). In a first layer, the fibers have a diameter of between 0.5 and 8 microns, in a second layer between 10 and 35 microns.
US2001/0309012 also describes a polymer multilayer filtering system which comprises at least two layers: a loading layer, where the fibers have a diameter of 5-30 microns and a basic weight of 30-100 g/m2, and an efficiency layer where the fibers have a diameter of 0.5-3 microns and a basic weight of 40-150 g/m2. In said multilayer, the object is achieved by using two-component fibers, i.e. comprising a portion of thermoplastic fibers having a certain melting point and a second portion of fibers having a lower melting point.
While the two filters described above solve the environmental problem, they do not reach the filtering efficiency and the accumulation capacity reached by the use of fiberglass.
In addition, in the fluid filtration field, and in particular in the field of filtration of liquids such as oils and fuels, there are substantial problems related to the formation of electrostatic charges.
Flowing through a non-conductive filtering material, as a polymer, ceramic and/or fiberglass material typically is, oils and fuels promote the formation of charge accumulations due to triboelectric effect. The electrostatic charge thus accumulated causes discharges which damage the integrity, efficiency and correct operation of the filter and, under certain conditions, can result in explosive phenomena. The frequency and magnitude of these phenomena depend on the features of the non-polar liquid, such as chemical composition, viscosity, presence of contaminants, and also on the environmental conditions of use of the liquid, temperature, relative humidity, pressure and velocity, and on the features of the hydraulic system.
The filtering materials produced as multilayer of non-woven fabric made from insulating thermoplastic polymer materials have a high volumetric and surface resistivity which promotes the formation and the accumulation of electrostatic charges.
In order to overcome this problem, U.S. Pat. No. 6,099,726 describes the introduction of metal meshes into the filtering system.
US 2009/0078637 describes metal or chemical surface coatings.
US 2011/0005990 describes surface treatments.
The object of the present invention is to provide a fully incinerable filtering system, i.e. entirely devoid of fiberglass, with high mechanical, chemical and physical resistance, as well as with antistatic properties and a high accumulation power with respect to the prior art for polymer filters having equal filtering efficiency.
A filtering multilayer is described, comprising at least two layers, one input layer and one output layer, made of non-woven fabric, wherein each fiber of said non-woven fabric consists of a polymer matrix of thermoplastic material, wherein the average diameter of the fibers that form the input layer is larger than the average diameter of the fibers that form the output layer, characterized in that the diameters of the fibers that form the input layer and the output layer have a Gaussian distribution, wherein the diameter of the single fibers that form said input layer varies around the average with a normal distribution of width at least equal to 10% of the average value and the diameter of the single fibers that form said output layer varies around the average with a normal distribution of width at least equal to 14% of the average value. In a preferred embodiment, said polymer matrix contains a carbon-based filler or additive, preferably in the form of powder.
The patent or application file may contain at least one drawing executed in color and/or one or more photographs. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee
The invention relates to a fully incinerable and preferably antistatic polymer filtering multilayer for filtering fluids.
The multilayer of the invention comprises at least two layers, one input layer and one output layer, made of non-woven fabric, wherein each fiber of said non-woven fabric consists of a polymer matrix of thermoplastic material, wherein the average diameter of the fibers that form the input layer is larger than the average diameter of the fibers that form the output layer, characterized in that the diameters of the fibers that form the input layer and the output layer have a Gaussian distribution. Preferably, each fiber of said non-woven fabric consists of a polymer matrix of thermoplastic material admixed with a carbon-based filler or additive, preferably in the form of powder.
The present invention describes and claims a filtering multilayer comprising at least two layers, one input layer and one output layer, made of non-woven fabric, wherein each fiber of said non-woven fabric consists of a polymer matrix of thermoplastic material, wherein the average diameter of the fibers that form the input layer is larger than the average diameter of the fibers that form the output layer, characterized in that the diameters of the fibers that form the input layer and the output layer have a Gaussian distribution, wherein the diameter of the single fibers that form said input layer varies around the average with a normal distribution of width at least equal to 10% of the average value and the diameter of the single fibers that form said output layer varies around the average with a normal distribution of width at least equal to 14% of the average value. Even more preferably, the diameter of the single fibers that form said input layer varies around the average with a normal distribution of width at least equal to 14% of the average value and the diameter of the single fibers that form said output layer varies around the average with a normal distribution of width at least equal to 19% of the average value.
In a preferred embodiment, the filtering multilayer of the present invention comprises at least two layers, wherein the average diameter of the fibers in said input layer is of between 6 and 15 μm and the distribution of the diameter of the single fibers that form said input layer varies around the average with a normal distribution of width at least equal to 14% of the average value, preferably of at least 15%; the average diameter of the fibers in said output layer is of between 1 and 6 μm, preferably between 3 and 5 μm and the distribution of the diameter of the single fibers that form said output layer varies around the average with a normal distribution of width at least equal to 19% of the average value, preferably of at least 20%.
Even more preferably, the average diameter of the fibers in said input layer is about 8 μm, with a normal distribution of width equal to 16% of the average value and the average diameter of the fibers in said output layer is about 3.6 μm, with a normal distribution of width equal to 22% of the average value.
The filtering multilayer of the present invention has a pressure drop of less than 7 kPa and an accumulation capacity greater than 19 mg/cm2. Said pressure drop and accumulation capacity data are intended as measured according to Multipass Test ISO16889 carried out according to the following parameters: 3 l/min flow rate, delta-P Terminal (at the end of the test) 500 kPa, sample made with flat disk having a filtering area of 102 cm2. All the pressure drop and accumulation capacity values shown in this description are intended as obtained by the aforementioned Multipass test ISO16889 and with the parameters mentioned above.
Further intermediate layers may optionally be provided between said input layer and said output layer. In this possible intermediate layers, the average diameter of the fibers decreases moving away from the input layer to the output layer.
In a further preferred embodiment, said multilayer comprises three layers, wherein the average diameter of the fibers in said input layer is about 8.2 μm, with a normal distribution of width of about 16% of the average value; the average diameter of the fibers in the intermediate layer is about 4.5 μm, with a normal distribution of width of about 16% of the average value and the average diameter of the fibers in said output layer is about 3.9 μm, with a normal distribution of width equal to about 22% of the average value.
In this embodiment, the multilayer has a mean flow pore size of about 18 μm, a filtering efficiency β1000 of about 10 μm(c), a pressure drop lower than 5 kPa and an accumulation capacity higher than 20 mg/cm2.
Said fibers forming the non-woven fabric used in the filtering multilayer of the present invention are preferably made of thermoplastic polyester, preferably they are made of PET, Nylon, polyesters, polycarbonate, polyethylenes, PBT or a mixture thereof. In a preferred embodiment, said fibers are made of PBT.
In a further embodiment, during the thermal process that leads to obtaining each of the non-woven fabric layers, at least one carbon-based filler or additive is dispersed into the polymer matrix, such as carbon black and graphite, in amounts of between 2-30% w/w. Said filler preferably is carbon black alone, with an average particle size of less than 50 nm, a surface area, as measured by the BET method, greater than 100 m2/g and a pore volume greater than 100 cm3/g.
The surface resistivity of the non-woven fabric multilayer of the present invention is lower than 1010Ω and the volumetric resistivity is lower than 1010 Ω-cm. In a preferred embodiment, the surface resistivity is of between 10^5 and 10^10Ω and the volumetric resistivity is of between 10^4 and 10^10 Ω-cm. Such resistivity parameters make the multilayer of the present invention fall within the definition of antistatic. Said volumetric and surface resistivity data are intended to be obtained according to the ASTM D257 standard. All the volumetric and surface resistivity values shown in this description are intended to be obtained by the above ASTM D257 standard.
The thickness of each of the at least two layers that form the multilayer of the present invention is in the range of between 0.05 and 3 mm, preferably between 0.2 and 2 mm, even more preferably it is between 0.3 and 1 mm.
By way of comparison, a single layer having a thickness of about 0.5 mm, wherein said fibers are of PBT and have an average diameter of about 8 μm, with a normal distribution with a width equal to about 16% of the average value, if used individually has an accumulation capacity of about 13 mg/cm2 and a filtering efficiency β1000 of 12 μm(c) or greater.
Again by way of comparison, a single layer having a thickness of about 0.5 mm, wherein said fibers are of PBT and have an average diameter of about 3.9 μm, with a normal distribution of width equal to about 22% of the average value, if used individually has an accumulation capacity of about 14 mg/cm2 and a filtering efficiency β1000 lower than 12 μn(c).
By joining said two layers in a multilayer according to the present invention, the multilayer obtained by joining said input layer and said output layer leads to an accumulation capacity equal to or greater than 20 mg/cm2 and to a filtering efficiency β1000 lower than 12 μm(c).
In a further embodiment, a method is claimed for obtaining a filtering multilayer according to the present invention, wherein said method comprises:
Providing a polymer fiber, wherein said polymer fiber is fully incinerable, with which a layer is prepared, possibly deposited on a support material, wherein the fibers in said layer have an average diameter of between 6 and 15 μm and the distribution of the diameter of the single fibers that form said layer varies about the average with a normal distribution of width at least equal to 10%, preferably 14% of the average value, even more preferably of at least 15%;
Providing a polymer fiber, wherein said fiber is fully incinerable and is of the same or of a different material with respect to the fiber in step a), with which a layer is prepared, possibly deposited on a support material, wherein the fibers in said layer have an average diameter of between 1 and 6 μm, preferably between 3 and 5 μm, and the distribution of the diameter of the single fibers that form said layer varies about the average with a normal distribution of width at least equal to 14%, preferably 19% of the average value, even more preferably of at least 20%.
Optionally, providing further layers as described in steps a) and b), wherein these further layers will form the intermediate layers of said multilayer and will be characterized by an average diameter of the fibers which decreases moving away from the input layer to the output layer.
Joining said layer obtained in a) with said layer obtained in b) and, optionally, with said further layers obtained in c).
It has been shown that in a multilayer system like that of the present invention the distribution of the diameter of the fibers that form the single layers plays a key role in determining not only the filtering efficiency but also the accumulation capacity of said filter.
The present invention provides filters which, while not containing fiberglass, have an accumulation capacity comparable to that so far obtainable only with the use of fiberglass. With the fibers made of a polymer matrix admixed with a carbon-based filler/additive, the formation and the accumulation of electrostatic charges is strongly limited, thus allowing a safe use of the filters of the present invention also for applications related to oil filtration in hydraulic systems and fuel filtration.
The multilayer, as a whole, has an approximate mean flow pore size of about 18 μm, a β1000 of about 12 μm(c), a pressure drop lower than 5 kPa and an accumulation capacity higher than 20 mg/cm2 (data obtained according to Multipass Test ISO16889 with the parameters shown above).
While the invention has been described with reference to various and preferred embodiments, it should be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the essential scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof.
Therefore, it is intended that the invention not be limited to the particular embodiment disclosed herein contemplated for carrying out this invention, but that the invention will include all embodiments falling within the scope of the claims.
Modina, Sergio, Indrieri, Marco, Speziali, Chantal Erika
| Patent | Priority | Assignee | Title |
| Patent | Priority | Assignee | Title |
| 8590712, | Oct 08 2008 | CUMMINS FILTRATION IP INC | Modular filter elements for use in a filter-in-filter cartridge |
| 20050067346, |
| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| May 19 2016 | Filtrec S.P.A. | (assignment on the face of the patent) | / | |||
| Jun 24 2016 | MODINA, SERGIO | FILTREC S P A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 039039 | /0843 | |
| Jun 24 2016 | INDRIERI, MARCO | FILTREC S P A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 039039 | /0843 | |
| Jun 24 2016 | SPEZIALI, CHANTAL ERIKA | FILTREC S P A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 039039 | /0843 |
| Date | Maintenance Fee Events |
| Feb 09 2022 | M2551: Payment of Maintenance Fee, 4th Yr, Small Entity. |
| Date | Maintenance Schedule |
| Aug 14 2021 | 4 years fee payment window open |
| Feb 14 2022 | 6 months grace period start (w surcharge) |
| Aug 14 2022 | patent expiry (for year 4) |
| Aug 14 2024 | 2 years to revive unintentionally abandoned end. (for year 4) |
| Aug 14 2025 | 8 years fee payment window open |
| Feb 14 2026 | 6 months grace period start (w surcharge) |
| Aug 14 2026 | patent expiry (for year 8) |
| Aug 14 2028 | 2 years to revive unintentionally abandoned end. (for year 8) |
| Aug 14 2029 | 12 years fee payment window open |
| Feb 14 2030 | 6 months grace period start (w surcharge) |
| Aug 14 2030 | patent expiry (for year 12) |
| Aug 14 2032 | 2 years to revive unintentionally abandoned end. (for year 12) |